US8586334B2 - Method for producing substance utilizing microorganism - Google Patents

Method for producing substance utilizing microorganism Download PDF

Info

Publication number
US8586334B2
US8586334B2 US09/897,988 US89798801A US8586334B2 US 8586334 B2 US8586334 B2 US 8586334B2 US 89798801 A US89798801 A US 89798801A US 8586334 B2 US8586334 B2 US 8586334B2
Authority
US
United States
Prior art keywords
ndh
strain
respiratory chain
energy efficiency
microorganism
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active, expires
Application number
US09/897,988
Other languages
English (en)
Other versions
US20020160461A1 (en
Inventor
Yuta Nakai
Kazuo Nakanishi
Yoshio Kawahara
Hisao Ito
Osamu Kurahashi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ajinomoto Co Inc
Original Assignee
Ajinomoto Co Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=18701548&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=US8586334(B2) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Ajinomoto Co Inc filed Critical Ajinomoto Co Inc
Assigned to AJINOMOTO CO., INC. reassignment AJINOMOTO CO., INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: ITO, HISAO, KAWAHARA, YOSHIO, KURAHASHI, OSAMU, NAKAI, YUTA, NAKANISHI, KAZUO
Publication of US20020160461A1 publication Critical patent/US20020160461A1/en
Priority to US14/055,302 priority Critical patent/US20140045219A1/en
Application granted granted Critical
Publication of US8586334B2 publication Critical patent/US8586334B2/en
Active legal-status Critical Current
Adjusted expiration legal-status Critical

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P1/00—Preparation of compounds or compositions, not provided for in groups C12P3/00 - C12P39/00, by using microorganisms or enzymes
    • C12P1/04—Preparation of compounds or compositions, not provided for in groups C12P3/00 - C12P39/00, by using microorganisms or enzymes by using bacteria
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P13/00—Preparation of nitrogen-containing organic compounds
    • C12P13/04—Alpha- or beta- amino acids
    • C12P13/22—Tryptophan; Tyrosine; Phenylalanine; 3,4-Dihydroxyphenylalanine
    • C12P13/222—Phenylalanine
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/0004—Oxidoreductases (1.)
    • C12N9/0012—Oxidoreductases (1.) acting on nitrogen containing compounds as donors (1.4, 1.5, 1.6, 1.7)
    • C12N9/0036—Oxidoreductases (1.) acting on nitrogen containing compounds as donors (1.4, 1.5, 1.6, 1.7) acting on NADH or NADPH (1.6)
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/0004—Oxidoreductases (1.)
    • C12N9/0012—Oxidoreductases (1.) acting on nitrogen containing compounds as donors (1.4, 1.5, 1.6, 1.7)
    • C12N9/0036—Oxidoreductases (1.) acting on nitrogen containing compounds as donors (1.4, 1.5, 1.6, 1.7) acting on NADH or NADPH (1.6)
    • C12N9/0038—Oxidoreductases (1.) acting on nitrogen containing compounds as donors (1.4, 1.5, 1.6, 1.7) acting on NADH or NADPH (1.6) with a heme protein as acceptor (1.6.2)
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P13/00—Preparation of nitrogen-containing organic compounds
    • C12P13/04—Alpha- or beta- amino acids
    • C12P13/08—Lysine; Diaminopimelic acid; Threonine; Valine
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P13/00—Preparation of nitrogen-containing organic compounds
    • C12P13/04—Alpha- or beta- amino acids
    • C12P13/22—Tryptophan; Tyrosine; Phenylalanine; 3,4-Dihydroxyphenylalanine

Definitions

  • the present invention relates to a method which uses a microorganism for producing a substance.
  • the microorganism is typically a bacteria belonging to the genus Escherichia , or coryneform bacteria, which are conventionally used for production of substances.
  • the substance to be produced may be selected from those conventionally produced by using microorganisms, for example, L-amino acids, nucleic acids, antibiotics, vitamins, growth factors, physiologically active substances, and so forth.
  • the present invention discloses means for improving production of final target substances in methods using microorganisms for producing substances.
  • This proton concentration gradient is the driving force of adenosine triphosphate (ATP) synthesis.
  • pathways of electron transfer include pathways showing high and low proton excretion ability, depending on the combination of NDH and oxidoreductases. It is thought that a pathway of high proton excretion ability shows high energy efficiency and a pathway of low proton excretion ability shows low energy efficiency.
  • one kind of microorganism simultaneously contains a plurality of respiratory chain electron transfer pathways in parallel, and those pathways include those of high energy efficiency and low energy efficiency.
  • NDH-1 encoded by the nuo operon
  • NDH-II encoded by ndh
  • cytochrome bo-type oxidase encoded by the cyoABCD operon
  • SoxM SoxM type
  • Corynebacterium glutamicum contains a cytochrome bc1 complex and at least two kinds of terminal oxidases, SoxM type oxidase and cytochrome bd type oxidase (The Second Symposium Concerning Metabolic Engineering, Lecture Abstracts, 1999).
  • the growth yield will be the lowest in the mutant strain having only the cytochrome bd-type oxidase, and it depends on the kind and energy acquisition efficiency of terminal oxidase (Annual Meeting of the Society for fermentation and Bioengineering Japan, 1995, Lecture Abstracts, No. 357).
  • an object of the present invention is to construct a microorganism showing improved energy efficiency and provide a method for producing a target substance by utilizing this method.
  • the inventors of the present invention conceived that a microorganism having an increased energy supply could be constructed by enhancing a respiratory chain pathway having high energy acquisition efficiency or making deficient a respiratory chain pathway showing low energy acquisition efficiency.
  • E. coli strains considered to have improved energy efficiency were prepared by amplifying a gene coding for cytochrome bo-type oxidase, a respiratory chain enzyme of high energy efficiency, or deleting a gene coding for NDH-II, a respiratory chain enzyme of low energy efficiency. Then, L-amino acid production was performed using these strains and it was found that the L-amino acid production was improved in strains whose energy efficiency was improved. Thus, the present invention was accomplished.
  • the present invention provides the following.
  • a method for producing a target substance utilizing a microorganism comprising culturing the microorganism in a medium to produce and cause accumulation of the target substance in the medium and collecting the target substance, wherein the microorganism is constructed from a parent strain of the microorganism having a respiratory chain pathway of high energy efficiency and a respiratory chain pathway of low energy efficiency as respiratory chain pathways, and the microorganism is a mutant strain or a genetic recombinant strain having either one or both of the following characteristics:
  • production of the target substance in a method utilizing a microorganism comprising culturing the microorganism in a medium to produce and cause accumulation of the target substance in the medium and collecting the target substance can be improved based on a novel principle.
  • FIG. 1 shows construction of plasmid pTS- ⁇ ndh for producing NDH-II gene-disrupted strain.
  • FIG. 2 shows construction of pMAN997.
  • the substance produced by the production method of the present invention is not particularly limited so long as it is a substance that can be produced by a microorganism.
  • examples thereof include L-amino acids such as L-threonine, L-lysine, L-glutamic acid, L-leucine, L-isoleucine, L-valine, and L-phenylalanine; nucleic acids such as guanylic acid and inosinic acid; vitamins; antibiotics; growth factors; physiologically active substances, and so forth.
  • the microorganism of the present invention is a microorganism having an ability to produce a target substance as described above, constructed from a parent strain of a microorganism having respiratory chain pathways of high and low energy efficiencies, and having either one or both of the following characteristics:
  • microorganisms including E. coli and coryneform bacteria contain a plurality of respiratory chain electron transfer pathways which function in parallel. These pathways include those which have high and low proton transfer value per electron.
  • E. coli for example, NDHI and NDHII as NADH dehydrogenase act as electron donors of NADH, and also catalyzes the proton transfer from NADH to the quinone pool.
  • NDHI shows high energy efficiency
  • NDHII shows low energy efficiency. That is, NDHII shows a molecular number of protons that can be excreted with one electron (proton transfer value) of 0, whereas that of NDHI is considered to be 2.
  • a pathway showing a high proton transfer value per electron as described above i.e., a respiratory chain pathway of high energy efficiency
  • a respiratory chain pathway of low energy efficiency is made deficient.
  • the respiratory chain pathway having high energy efficiency can be enhanced by enhancing the activity of a respiratory chain enzyme involved in the respiratory chain pathway.
  • the respiratory chain pathway of low energy efficiency can be made deficient by reducing or eliminating the activity of a respiratory chain enzyme involved in the respiratory chain pathway.
  • the respiratory chain enzyme involved in a respiratory chain pathway is not particularly limited so long as it is an enzyme constituting the respiratory chain pathway.
  • examples thereof include dehydrogenases that catalyze electron transfer from an electron donor to a quinone pool such as ubiquinone, dimethylmenaquinone, and menaquinone, and oxidases that catalyze electron transfer from a quinone pool to an electron donor.
  • the oxidases that catalyze a reaction producing a water molecule by electron transfer from a quinone pool are classified as SoxM type (bo-type) and bd-type.
  • SoxM type bo-type
  • bd-type The proton transfer value of the bo-type is 2, whereas that of the bd-type is 1. Therefore, the bo-type shows higher energy efficiency.
  • a recombinant DNA can be prepared by ligating a gene fragment coding for the enzyme to a vector which functions in the microorganism, preferably a multi-copy type vector, and introducing the ligated vector into the microorganism.
  • the copy number of the gene coding for the enzyme in the transformed strain is thereby increased, and as a result, the enzymatic activity is amplified.
  • This procedure will be explained below in the example section showing that the cyo operon (cyoABCDE) codes for a cytochrome bo-type oxidase, which is a respiratory chain enzyme of high energy efficiency.
  • a plasmid autonomously replicable in E. coli cells can be used as a vector in gene cloning and for introduction of gene into a microorganism, for example. Specific examples thereof include pUC19, pUC18, pBR322, pHSG299, pHSG298, pHSG399, pHSG398, RSF1010, pSTV29 and so forth.
  • a shuttle vector autonomously replicable in coryneform bacteria and E. coli can preferably be used for gene introduction into coryneform bacteria. Examples of plasmids autonomously replicable in coryneform bacteria are listed below
  • the vector is first digested with a restriction enzyme compatible with the ends of the cyo operon.
  • the ligation is usually performed by a ligase such as T4 DNA ligase.
  • any known transformation method can be employed. For instance, a method of treating recipient cells with calcium chloride so as to increase the permeability of DNA has been reported for E. coli K-12 (Mandel, M. and Higa, A., J. Mol. Biol., 53, 159 (1970)). Also, a method of preparing competent cells from cells at the growth phase, followed by introducing the DNA thereinto has been reported for Bacillus subtilis (Duncan, C. H., Wilson, G. A. and Young, F. E., Gene, 1, 153 (1977)).
  • the amplification of cytochrome bo-type oxidase activity can also be attained by allowing multiple copies of the cyo operon to exist on the host's chromosomal DNA.
  • a microorganism such as bacteria belonging to the genus Escherichia and coryneform bacteria
  • homologous recombination is carried out using a sequence having multiple copies as targets on the chromosomal DNA.
  • Repetitive DNA, or inverted repeats at the end of a transposable element can be used as sequences whose multiple copies exist in the chromosomal DNA.
  • enhancing the cytochrome bo-type oxidase activity can also be attained by replacing an expression regulatory sequence of cyo operon, such as a promoter, with a stronger promoter (see Japanese Patent Unexamined Publication No. 1-215280).
  • a promoter such as a promoter
  • lac promoter, lip promoter, trc promoter, tac promoter, P R promoter and P L , promoter of lambda phage, tet promoter, amyE promoter, and so forth are known as strong promoters. Substitution of these promoters enhances expression of the cyo operon, and hence the cytochrome bo-type oxidase activity is enhanced.
  • the method of enhancing an expression regulatory sequence may be combined with a method of increasing the copy number of the cyo operon.
  • the enhancement of activity of a respiratory chain enzyme of high energy efficiency can also be attained by introducing a mutation via mutagenesis of the microorganism that results in increasing the intracellular activity of the enzyme.
  • a mutation include mutations of the coding region increasing the specific activity of the enzyme, mutations in the expression regulatory sequences increasing expression of the gene, and so forth.
  • Methods utilizing treatment by ultraviolet irradiation or treatment with a known mutagenesis agent such as N-methyl-N′-nitro-N-nitrosoguanidine (NTG) and nitrous acid can be used as the mutagenesis treatment.
  • a mutation is introduced into the gene of the enzyme so that the intracellular activity of the enzyme is reduced or eliminated, or the gene on the chromosome of the microorganism is disrupted so that the gene does not function normally.
  • the method of disrupting the ndh gene will be explained in the examples section, which shows ndh coding for NDH-II as a gene of a respiratory chain enzyme of low energy efficiency.
  • ndh of E. coli has been reported (Young et al., European Journal of Biochemistry, 116:165-170 (1981)), and therefore the gene can be cloned based on the reported sequence. It is also possible to use a ndh gene derived from a bacterium belonging to the genus Escherichia , or derived from other organisms such as coryneform bacteria.
  • a ndh gene on the chromosome can be disrupted by transforming a microorganism with DNA containing a ndh gene modified with an internal deletion so as to not produce a functional NDH-II (deletion-type ndh gene), and allowing recombination between the deletion-type ndh gene and the ndh gene on the chromosome.
  • Gene destruction by homologous recombination has already been established, and there are methods utilizing a linear DNA, a plasmid that contains a temperature-sensitive replication control region, and so forth. In the present invention, the method utilizing a plasmid that contains a temperature-sensitive replication control region is preferred.
  • a ndh gene on the host chromosome can be replaced with the deletion-type ndh gene as follows.
  • a microorganism is transformed with a recombinant DNA prepared by inserting a temperature-sensitive replication control region, deletion-type ndh gene, and marker gene for resistance to a drug.
  • the resulting transformed strain is cultured at a temperature at which the temperature-sensitive replication control region does not function, and then the transformed strain can be cultured in a medium containing the drug, which results in obtaining a transformed strain in which the recombinant DNA is incorporated into the chromosomal DNA.
  • the deletion-type ndh gene is recombined with the ndh gene originally present on the chromosome, and the two fusion chromosomal ndh-deletion-type ndh genes are inserted into the chromosome so that the other portions of the recombinant DNA (vector segment, temperature-sensitive replication control region and drug resistance marker) are present between the two fusion genes. Therefore, the transformant expresses NDH-II, because the normal ndh gene is dominant in this state.
  • the deletion-type ndh gene is eliminated together with the vector segment (including the temperature-sensitive replication control region and the drug resistance marker) from the chromosomal DNA by recombination of the two ndh genes.
  • the normal ndh gene is left on the chromosomal DNA, and the deletion-type ndh gene is excised from the chromosomal DNA.
  • the deletion-type ndh gene can be left on the chromosomal DNA, and the normal ndh gene can be excised from the chromosome DNA.
  • the excised DNA may be retained in the cell as a plasmid when the cell is cultured at a temperature at which the temperature-sensitive replication control region can function. Subsequently, the cell is cultured at a temperature at which the temperature-sensitive replication control region cannot function, resulting indropping out the plasmid DNA, and ndh gene deletion mutant can be obtained.
  • Examples of the vector having a temperature-sensitive replication origin for E. coli include, for example, the plasmid pMAN997 described in International Patent Publication WO99/03988, and so forth.
  • Examples of the vector having a temperature-sensitive replication origin for coryneform bacteria include, for example, the plasmid pHSC4 disclosed in Japanese Patent Unexamined Publication No. 5-7491, and so forth.
  • the plasmids are not limited to these, and other vectors can also be used.
  • microorganisms obtained as described above include microorganisms wherein one or both of SoxM type oxidase or NDH-1 is enhanced, microorganisms wherein the activities of one or both of cytochrome bd-type oxidase or NDH-II are reduced or eliminated, and microorganism wherein one or both of SoxM type oxidase or NDH-1 are enhanced, and wherein activities of one or both of cytochrome bd type oxidase or NDH-II are reduced or eliminated. More specifically, there can be mentioned, for example, E. coli wherein the activity of SoxM type oxidase is enhanced and the activity of NDH-II is made deficient. Examples of SoxM type oxidase include cytochrome bo-type oxidase.
  • the microorganism used for the present invention is not particularly limited so long as it can be imparted with the aforementioned properties, and examples thereof include bacteria belonging to the genus Escherichia such as E. coli , coryneform bacteria such as Brevibacterium lactofermentum ( Corynebacterium glutamicum ), Bacillus bacteria such as Bacillus subtilis, Serratia bacteria such as Serratia marcescens , yeast such as Saccharomyces cerevisae , and so forth.
  • bacteria belonging to the genus Escherichia such as E. coli
  • coryneform bacteria such as Brevibacterium lactofermentum ( Corynebacterium glutamicum )
  • Bacillus bacteria such as Bacillus subtilis
  • Serratia bacteria such as Serratia marcescens
  • yeast such as Saccharomyces cerevisae , and so forth.
  • the activity of an enzyme involved in biosynthesis of the target substance may be enhanced, depending on the target substance. Furthermore, the activity of an enzyme disadvantageous for the production of the target substance may be reduced or eliminated.
  • a target substance can be produced by culturing such a microorganism as described above in a medium to produce and cause accumulation of the target substance in the medium, and collecting the target substance.
  • the medium used for the production of a target substance may be a conventionally used well-known medium and can be selected depending on the microorganism to be utilized. That is, the medium may be a usual medium containing a carbon source, nitrogen source, inorganic ions, as well as other organic components, if necessary. A special medium is not required for practicing the present invention.
  • sugars such as glucose, lactose, galactose, fructose or starch hydrolysate; alcohols such as glycerol or sorbitol; organic acids such as fumaric acid, citric acid or succinic acid, and so forth.
  • the nitrogen source it is possible to use inorganic ammonium salts such as ammonium sulfate, ammonium chloride or ammonium phosphate; organic nitrogen such as soybean hydrolysate; ammonia gas; aqueous ammonia, and so forth.
  • inorganic ammonium salts such as ammonium sulfate, ammonium chloride or ammonium phosphate
  • organic nitrogen such as soybean hydrolysate
  • ammonia gas aqueous ammonia, and so forth.
  • the medium it is desirable for the medium to contain required substances such as vitamin B 1 , L-homoserine, and L-tyrosine, or yeast extract in appropriate amounts as organic trace nutrients.
  • required substances such as vitamin B 1 , L-homoserine, and L-tyrosine, or yeast extract in appropriate amounts as organic trace nutrients.
  • potassium phosphate, magnesium sulfate, iron ion, manganese ion, and so forth are added in small amounts, if necessary.
  • the culture can be performed under conventional well-known conditions and can be selected according to a microorganism to be utilized.
  • the culture is preferably performed under aerobic conditions for 16-120 hours.
  • the culture temperature is preferably maintained at 25° C. to 45° C.
  • pH is preferably maintained at 5-8 during the culture.
  • Inorganic or organic, acidic or alkaline substances as well as ammonia gas, or the like can be used for pH adjustment.
  • the present invention can be practiced by using a combination of conventional well-known ion exchange techniques, precipitation techniques and other techniques.
  • the target cyo operon gene was obtained from the phage library of Kohara (Kohara et al., Cell, 50:495-508 (1987)) containing the cyo operon.
  • Phage DNA was obtained from the phage clone 147[2H5] of Kohara containing the operon using Wizard lambda prep (Promega).
  • the obtained phage DNA 147[2H5] was digested with PshBI, and the obtained 5.5 kb fragment containing the cyo operon was blunt-ended, and inserted into the SmaI site of pMW119 (Nippon Gene) to clone the cyo operon containing a promoter region.
  • the cyo operon was inserted in the reverse direction with respect to the lactose operon promoter on pMW119. This plasmid was designated pMW(CYO)B.
  • the plasmid pMW(CYO)B was introduced into E. coli W3110 strain (obtained from the National Institute of Genetics, Mishima, Shizuoka, Japan) to obtain W3110/pMW(CYO)B.
  • Ubiquinol oxidase activity present in the cell extracts of W3110 and W3110/pMW(CYO)B strains was measured as terminal oxidase activity by using a known method (Kita et al., The Journal of Biological Chemistry, 259:3368-3374 (1984)). The results are shown in Table 1.
  • terminal oxidase activity was enhanced in the strain introduced with pMW(CYO)B as shown in Table 1. This enhancement of the terminal oxidase activity is considered to be caused by the enhancement of cytochrome bo-type oxidase activity through the enhancement of cyo operon.
  • NDH-II deficient strain In order to produce a NDH-II deficient strain, an internally cleaved partial sequence of NDH-II (disrupted type NDH-II gene) was prepared. The partial sequence of NDH-II was cloned based on the known sequence of the gene ndh coding for NDH-II of E. coli (Young et al., European Journal of Biochemistry, 116:165-170 (1981)).
  • the disrupted type NDH-II gene was produced as follows ( FIG. 1 ). First, a DNA fragment of about 2.4 kb containing the partial sequence of NDH-II was amplified from E. coli chromosomal DNA by PCR using ndh-1 (SEQ ID NO: 1) and ndh-2 (SEQ ID NO: 2) as primers. This fragment was cloned into pGEM-T vector (Promega) to obtain pGEM-ndh.
  • This pGEM-ndh was digested with restriction enzymes EcoRI and StuI, and the obtained DNA fragment of 0.5 kb was collected and ligated to pTWV229 (Takara Shuzo), which had been digested with EcoRI and SmaI, to obtain pTWV-ndh.
  • pGEM-ndh was digested with a restriction enzyme StuI, and the obtained DNA fragment of 0.9 kb was collected and inserted into the HincII site of pTWV-ndh.
  • pTWV ⁇ ndh was obtained containing a part of the multi-cloning sites of pTWV229 in the partial sequence of ndh.
  • the plasmid pTWV ⁇ ndh contained the ndh sequence inserted with a sequence of 17 bp derived from pTWV229 at the StuI site in the ndh sequence.
  • Homologous recombination was performed between this plasmid pTS- ⁇ ndh and the genome of W3110 strain as for ndh by a usual homologous recombination technique utilizing the temperature sensitivity of pTS- ⁇ ndh (Matuyama et al., Journal of Bacteriology, 162:1196 (1985)) to obtain a W3110(ndh) strain that did not express normal NDH-II protein because the sequence of 17 bp derived from pTWV229 was inserted in the coding region of ndh on the genome.
  • tyrA deficiency was introduced into the W3110(ndh) strain by P1 transduction using tetracycline resistance as a marker to obtain a W3110(ndh, tyrA) strain.
  • the aforementioned pMAN997 was obtained by exchanging the VspI-HindIII fragments of pMAN031 ( J. Bacteriol, 162, 1196 (1985)) and pUC19 (Takara Shuzo) ( FIG. 2 ).
  • the E. coli W3110 strain was obtained from the National Institute of Genetics (Mishima, Shizuoka). This strain was seeded on an LB plate containing streptomycin, and a strain that formed a colony was selected to obtain a streptomycin-resistant strain. The selected streptomycin resistant strain and E. coli K-12 ME8424 strain were mixed, and cultured in a complete medium (L-Broth: 1% Bacto trypton, 0.5% Yeast extract, 0.5% NaCl) at 37° C. for 15 minutes as stationary culture to induce conjugation. The E.
  • coli K-12 ME8424 strain has the genetic traits of (HfrPO45, thi, relA1, tyrA::Tn10, ung-1, nadB), and it can be obtained from the National Institute of Genetics. Thereafter, the culture was seeded in a complete medium (L-Broth: 1% Bacto trypton, 0.5% Yeast extract, 0.5% NaCl, 1.5% agar) containing streptomycin, tetracycline and L-tyrosine, and a strain that formed a colony was selected. This strain was designated as E. coli W3110(tyrA) strain.
  • European Patent Unexamined Publication No. 488424/1992 discloses many strains obtained by introducing a plasmid into the above strain.
  • a strain obtained by introducing a plasmid pHATerm was designated as E. coli W3110(tyrA)/pHATerm, deposited on Nov.
  • the E. coli W3110(tyrA) strain can be obtained by eliminating the plasmid pHATerm from the above strain in a conventional manner.
  • the plasmid pMW(CYO)B obtained in Example 1 was introduced into the W3110(tyrA) strain and the W3110(ndh, tyrA) strain obtained in Example 2 to obtain W3110(tyrA)/pMW(CYO)B and W3110(ndh, tyrA)/pMW(CYO)B, respectively.
  • pMW119 was introduced into W3110(tyrA) to obtain W3110(tyrA)/pMW119 strain.
  • the medium was adjusted to pH 7.0 with KOH, and autoclaved at 115° C. for 10 minutes. However, glucose and MgSO 4 .7H 2 O were sterilized separately. Further, before the culture, 30 g/L of CaCO 3 (Japanese Pharmacopoeia), which was subjected to dry sterilization at 180° C., and 100 ⁇ g/L of an antibiotics, ampicillin, were added to the medium.
  • CaCO 3 Japanese Pharmacopoeia
  • L-lysine productivity was improved in the E. coli producing L-lysine by enhancing the cytochrome bo-type oxidase activity. This is considered to be caused because energy acquisition efficiency was improved by enhancement of the respiratory chain pathway of high energy efficiency, and the energy was used for the L-lysine production.
  • the plasmid pMW(CYO)B obtained by the aforementioned method was introduced into an L-threonine producing bacterium, E. coli VKPM B-3996 (RIA 1867) (refer to U.S. Pat. No. 5,175,107, hereafter referred to as “B-3996” strain) to obtain B-3996/pMW(CYO)B strain.
  • the B-3996 strain harbored a plasmid pVIC40 (International Patent Publication WO90/04636) obtained by inserting the threonine operon into a wide host-range vector plasmid pAYC32 containing a streptomycin resistance marker (refer to Chistorerdov, A. Y., Tsygankov, Y. D., Plasmid, 1986, 16, 161-167).
  • the B-3996 strain was deposited at USSR Antibiotics Research Institute (VNIIA) under a registration number of RIA1867.
  • B-3996/pMW119 was obtained by introducing pMW119 into B-3996.
  • the L-threonine productivity of these B-3996/pMW(CYO)B and B-3996/pMW119 was evaluated by culture in flask. The culture was performed by using a medium having the composition mentioned in Table 3 at a temperature of 37° C. for 38 hours with stirring at 114-116 rpm.
  • Component A, Component B and Component C mentioned in Table 3 were prepared and sterilized separately, and then they were cooled and mixed in a ratio of 16/20 volume of Component A, 4/20 volume of Component B and 30 g/L, of Component C. The results are shown in Table 4.
  • Threonine production medium A (NH 4 ) 2 SO 4 16 g/L KH 2 PO 4 1 g/L FeSO 4 .7H 2 O 0.01 g/L MnSO 4 .4H 2 O 0.01 g/L Yeast Extract (Difco) 2 g/L L-Isoleucine 50 mg/L Nicotinic acid 10 mg/L Adjusted to pH 7.0 with KOH and autoclaved at 115° C. for 10 minute (16/20 volume) B 20% glucose autoclaved at 115° C. for 10 minute (4/20 volume) MgSO 4 .7H 2 O 1 g/L C CaCO 3 according to Japanese Pharmacopoeia, subjected to dry sterilization at 180° C. (30 g/L) Antibiotics (100 ⁇ g/L of streptomycin and 5 ⁇ g/L of kanamycin)
  • a plasmid pACMAB was collected from the E. coli W3110(tyrA)/pACMAB, pBR-aroG4 strain according to a usual purification method for a plasmid.
  • the plasmid was obtained by inserting a DNA fragment containing a gene for desensitized-type chorismate mutase/prephenate dehydratase (CM-PDH) in the proper L-phenylalanine biosynthesis system between the BamHI and HindIII cleavage sites of the plasmid vector pACYC184 (Ap r ) (refer to International Patent Publication WO97/08333).
  • CM-PDH desensitized-type chorismate mutase/prephenate dehydratase
  • the W3110(tyrA)/pACMAB, pBR-aroG4 strain (designated as AJ12604) was deposited on Jan. 28, 1991 at the National Institute of Bioscience and Human-Technology, Agency of Industrial Science and Technology, Ministry of International Trade and Industry (1-3 Higashi 1-Chome, Tsukuba-shi, Ibaraki-ken, Japan, postal code: 305) and received an accession number of FERM P-11975. Then, it was converted to an international deposit under the provisions of the Budapest Treaty on Sep. 26, 1991, and received an accession number of FERM BP-3579.
  • the plasmid pACMAB was blunt-ended by digestion with SalI. Into this, a blunt-ended DNA fragment containing the cyo operon of 5.5 kb, which was obtained from the aforementioned phage DNA 147[2H5] of Kohara by digestion with PshBI, was inserted. The obtained plasmid pACMAB-cyo was introduced into W3110(tyrA/pBR-aroG4).
  • the obtained transformant strain was cultured in a medium for L-phenylalanine production (containing 20 g of glucose, 29.4 g of disodium hydrogenphosphate, 6 g of potassium dihydrogenphosphate, 1 g sodium chloride, 2 g of ammonium chloride, 10 g of sodium citrate, 0.4 g of sodium glutamate, 3 g of magnesium sulfate heptahydrate, 0.23 g of calcium chloride, 2 mg of thiamin hydrochloride, and 100 mg of L-tyrosine in 1 L of water, pH 7.0) at 37° C. for 40 hours.
  • L-Phenylalanine contained in the medium was quantified by high performance liquid chromatography. The results are shown in Table 5.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Genetics & Genomics (AREA)
  • Biotechnology (AREA)
  • Microbiology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Molecular Biology (AREA)
  • Biomedical Technology (AREA)
  • Mycology (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Medicines Containing Material From Animals Or Micro-Organisms (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Enzymes And Modification Thereof (AREA)
US09/897,988 2000-07-05 2001-07-05 Method for producing substance utilizing microorganism Active 2025-07-08 US8586334B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US14/055,302 US20140045219A1 (en) 2000-07-05 2013-10-16 Method for Producing Substance Utilizing Microorganism

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2000-204252 2000-07-05
JP2000204252A JP4380029B2 (ja) 2000-07-05 2000-07-05 微生物を利用した物質の製造法

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US14/055,302 Continuation US20140045219A1 (en) 2000-07-05 2013-10-16 Method for Producing Substance Utilizing Microorganism

Publications (2)

Publication Number Publication Date
US20020160461A1 US20020160461A1 (en) 2002-10-31
US8586334B2 true US8586334B2 (en) 2013-11-19

Family

ID=18701548

Family Applications (2)

Application Number Title Priority Date Filing Date
US09/897,988 Active 2025-07-08 US8586334B2 (en) 2000-07-05 2001-07-05 Method for producing substance utilizing microorganism
US14/055,302 Abandoned US20140045219A1 (en) 2000-07-05 2013-10-16 Method for Producing Substance Utilizing Microorganism

Family Applications After (1)

Application Number Title Priority Date Filing Date
US14/055,302 Abandoned US20140045219A1 (en) 2000-07-05 2013-10-16 Method for Producing Substance Utilizing Microorganism

Country Status (16)

Country Link
US (2) US8586334B2 (pt)
EP (2) EP1170376B1 (pt)
JP (1) JP4380029B2 (pt)
KR (1) KR100805644B1 (pt)
CN (1) CN1280419C (pt)
AT (2) ATE501265T1 (pt)
AU (1) AU782560B2 (pt)
BR (1) BRPI0102666B1 (pt)
DE (2) DE60144205D1 (pt)
DK (2) DK2067864T3 (pt)
ES (2) ES2331601T3 (pt)
MY (1) MY127434A (pt)
PE (1) PE20020172A1 (pt)
PL (1) PL206590B1 (pt)
RU (1) RU2238325C2 (pt)
TW (1) TWI238192B (pt)

Families Citing this family (94)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2175351C2 (ru) 1998-12-30 2001-10-27 Закрытое акционерное общество "Научно-исследовательский институт "Аджиномото-Генетика" (ЗАО "АГРИ") Фрагмент днк из escherichia coli, определяющий повышенную продукцию l-аминокислот (варианты), и способ получения l-аминокислот
JP2001046067A (ja) * 1999-08-04 2001-02-20 Ajinomoto Co Inc 好熱性バチルス属細菌由来のｌ−リジン生合成系遺伝子
PL341895A1 (en) * 1999-08-12 2001-02-26 Ajinomoto Kk Plasmide autonomously replicable in corynebacter bacteria
BRPI0016995B1 (pt) * 2000-01-21 2016-03-08 Ajinomoto Kk bactéria escherichia coli geneticamente modificada, e, método para produzir l-lisina
WO2003072785A2 (en) * 2002-02-27 2003-09-04 Dsm Ip Assets B.V. Fermentation process
WO2004033421A2 (en) 2002-10-04 2004-04-22 Genencor International, Inc. Improved production of bacterial strains
KR101148255B1 (ko) 2002-10-04 2012-08-08 다니스코 유에스 인크. 고수율을 갖는 1,3-프로판디올의 생물학적 제조 방법
BR0304860A (pt) * 2002-11-11 2004-08-31 Ajinomoto Kk Método para produzir uma substância alvo pela utilização de uma-bactéria pertencente ao gênero escherichia
DE10254074A1 (de) * 2002-11-19 2004-06-17 Forschungszentrum Jülich GmbH Verfahren zur mikrobiellen Herstellung von Stoffwechselprodukten
MXPA05008857A (es) * 2003-02-18 2006-03-09 Metabolic Explorer Sa Procedimiento de preparacion de microorganismos evolucionados que permite la creacion o la modificacion de vias metabolicas.
US7335496B2 (en) * 2003-06-05 2008-02-26 Ajinomoto Co., Inc. Method for producing target substance
PL1651758T3 (pl) * 2003-07-29 2009-04-30 Ajinomoto Kk Sposób wytwarzania L-lizyny lub L-treoniny przy użyciu bakterii Escherichia o atenuowanej aktywności enzymu jabłczanowego
FR2862068B1 (fr) * 2003-11-06 2007-10-12 Metabolic Explorer Sa Souches de microorganismes optimisees pour des voies de biosyntheses consommatrices de nadph
JP4380305B2 (ja) * 2003-11-21 2009-12-09 味の素株式会社 発酵法によるｌ−アミノ酸の製造法
PL1664318T3 (pl) * 2004-01-30 2010-03-31 Ajinomoto Kk Mikroorganizm wytwarzający L-aminokwas i sposób wytwarzania L-aminokwasu
JP4780783B2 (ja) * 2004-02-27 2011-09-28 協和発酵バイオ株式会社 アミノ酸の製造法
US7344874B2 (en) * 2004-03-04 2008-03-18 Ajinomoto Co., Inc. L-glutamic acid-producing microorganism and a method for producing L-glutamic acid
US7300776B2 (en) 2004-04-26 2007-11-27 Ajinomoto Co., Inc. L-amino acid-producing bacterium and a method for producing L-amino acid
US7482140B2 (en) * 2004-06-15 2009-01-27 Ajinomoto Co., Inc. L-tyrosine-producing bacterium and a method for producing L-tyrosine
US7205132B2 (en) * 2004-09-10 2007-04-17 Ajinomoto Co., Inc. L-glutamic acid-producing microorganism and a method for producing L-glutamic acid
US7794989B2 (en) * 2004-12-28 2010-09-14 Ajinomoto Co., Inc. L-glutamic acid-producing microorganism and a method for producing L-glutamic acid
US7547531B2 (en) 2005-01-18 2009-06-16 Ajinomoto Co., Inc. L-amino acid producing microorganism which has been modified to inactive the fimH gene, and a method for producing I-amino acid
JP4985407B2 (ja) * 2005-05-30 2012-07-25 味の素株式会社 ポリ−γ−グルタミン酸の製造法及びその製造法に用いられる微生物
US20070004014A1 (en) * 2005-06-29 2007-01-04 Yuichiro Tsuji Method for producing l-threonine
JP2008283863A (ja) 2005-08-26 2008-11-27 Ajinomoto Co Inc Ｌ−アミノ酸生産菌及びｌ−アミノ酸の製造方法
JP2007185184A (ja) * 2005-12-16 2007-07-26 Ajinomoto Co Inc Ｌ−アミノ酸生産菌及びｌ−アミノ酸の製造法
EP1979486B1 (en) 2006-01-30 2013-04-17 Ajinomoto Co., Inc. L-amino acid producing bacterium and method of producing l-amino acid
JP2009095237A (ja) * 2006-02-02 2009-05-07 Ajinomoto Co Inc Ｌ−アミノ酸の製造法
JP2009118740A (ja) * 2006-03-03 2009-06-04 Ajinomoto Co Inc Ｌ−アミノ酸の製造法
WO2007119574A2 (en) 2006-03-23 2007-10-25 Ajinomoto Co., Inc. A method for producing an l-amino acid using bacterium of the enterobacteriaceae family with attenuated expression of a gene coding for small rna
JP2009060791A (ja) 2006-03-30 2009-03-26 Ajinomoto Co Inc Ｌ−アミノ酸生産菌及びｌ−アミノ酸の製造法
JP2009165355A (ja) 2006-04-28 2009-07-30 Ajinomoto Co Inc Ｌ−アミノ酸を生産する微生物及びｌ−アミノ酸の製造法
KR101109402B1 (ko) 2006-05-09 2012-01-30 미쓰이 가가쿠 가부시키가이샤 보효소 재생에 의한 히드록시카르복실산류의 생산방법
JP4954985B2 (ja) * 2006-05-09 2012-06-20 三井化学株式会社 補酵素合成強化によるグリコール酸の生産方法
WO2007136133A1 (en) 2006-05-23 2007-11-29 Ajinomoto Co., Inc. A method for producing an l-amino acid using a bacterium of the enterobacteriaceae family
JP5407858B2 (ja) * 2006-07-19 2014-02-05 味の素株式会社 腸内細菌科の細菌を用いたｌ−アミノ酸の製造方法
US20080293101A1 (en) * 2006-07-27 2008-11-27 Peters Matthew W Engineered microorganisms for increasing product yield in biotransformations, related methods and systems
US9562224B2 (en) * 2006-09-07 2017-02-07 William Marsh Rice University Reduced activity of ubiCA in E. coli
JP2010017081A (ja) * 2006-10-10 2010-01-28 Ajinomoto Co Inc Ｌ−アミノ酸の製造法
WO2008072761A2 (en) * 2006-12-11 2008-06-19 Ajinomoto Co., Inc. Method for producing an l-amino acid
RU2006143864A (ru) 2006-12-12 2008-06-20 Закрытое акционерное общество "Научно-исследовательский институт Аджиномото-Генетика" (ЗАО АГРИ) (RU) СПОСОБ ПОЛУЧЕНИЯ L-АМИНОКИСЛОТ С ИСПОЛЬЗОВАНИЕМ БАКТЕРИИ СЕМЕЙСТВА ENTEROBACTERIACEAE, В КОТОРОЙ ОСЛАБЛЕНА ЭКСПРЕССИЯ ГЕНОВ cynT, cynS, cynX, ИЛИ cynR, ИЛИ ИХ КОМБИНАЦИИ
RU2006145712A (ru) * 2006-12-22 2008-06-27 Закрытое акционерное общество "Научно-исследовательский институт Аджиномото-Генетика" (ЗАО АГРИ) (RU) Способ получения l-аминокислот методом ферментации с использованием бактерий, обладающих повышенной способностью к утилизации глицерина
CN101627110B (zh) 2007-01-22 2014-08-13 味之素株式会社 生产l-氨基酸的微生物和l-氨基酸的生产方法
JP2010088301A (ja) * 2007-02-01 2010-04-22 Ajinomoto Co Inc Ｌ−アミノ酸の製造法
JP2010110217A (ja) 2007-02-22 2010-05-20 Ajinomoto Co Inc Ｌ−アミノ酸生産菌及びｌ−アミノ酸の製造法
JP2010226956A (ja) * 2007-07-23 2010-10-14 Ajinomoto Co Inc Ｌ−リジンの製造法
CN101939412B (zh) 2007-09-04 2016-01-20 味之素株式会社 生产氨基酸的微生物以及氨基酸的生产方法
JP2010263790A (ja) * 2007-09-04 2010-11-25 Ajinomoto Co Inc アミノ酸生産微生物及びアミノ酸の製造法
RU2395579C2 (ru) * 2007-12-21 2010-07-27 Закрытое акционерное общество "Научно-исследовательский институт Аджиномото-Генетика" (ЗАО АГРИ) СПОСОБ ПОЛУЧЕНИЯ L-АМИНОКИСЛОТЫ С ИСПОЛЬЗОВАНИЕМ БАКТЕРИИ, ПРИНАДЛЕЖАЩЕЙ К РОДУ Escherichia
JP2011067095A (ja) 2008-01-10 2011-04-07 Ajinomoto Co Inc 発酵法による目的物質の製造法
EP2248906A4 (en) 2008-01-23 2012-07-11 Ajinomoto Kk PROCESS FOR THE PREPARATION OF L-AMINO ACID
RU2008105793A (ru) 2008-02-19 2009-08-27 Закрытое акционерное общество "Научно-исследовательский институт Аджиномото-Генетика" (ЗАО АГРИ) (RU) Способ конструирования оперонов, содержащих трансляционно сопряженные гены, бактерия, содержащая такой оперон, способ продукции полезного метаболита и способ мониторинга экспрессии гена
JP2011167071A (ja) 2008-05-22 2011-09-01 Ajinomoto Co Inc Ｌ−アミノ酸の製造法
EP2336347B1 (en) 2008-09-08 2017-03-15 Ajinomoto Co., Inc. An l-amino acid-producing microorganism and a method for producing an l-amino acid
KR101123213B1 (ko) * 2008-09-11 2012-03-19 부산대학교 산학협력단 미생물 전자전달계 및 탄소원 대사경로가 재설계된 재조합 대장균 생촉매
JP2012029565A (ja) 2008-11-27 2012-02-16 Ajinomoto Co Inc Ｌ−アミノ酸の製造法
JP2010142200A (ja) 2008-12-22 2010-07-01 Ajinomoto Co Inc Ｌ−リジンの製造法
BRPI1007069A2 (pt) 2009-01-23 2015-08-25 Ajinomoto Kk Método para produzir um l-aminoácido.
JP5521347B2 (ja) 2009-02-16 2014-06-11 味の素株式会社 Ｌ−アミノ酸生産菌及びｌ−アミノ酸の製造法
JPWO2011013707A1 (ja) 2009-07-29 2013-01-10 味の素株式会社 Ｌ−アミノ酸の製造法
JP2012223092A (ja) 2009-08-28 2012-11-15 Ajinomoto Co Inc Ｌ−アミノ酸の製造法
JP2013013329A (ja) 2009-11-06 2013-01-24 Ajinomoto Co Inc Ｌ−アミノ酸の製造法
RU2460793C2 (ru) 2010-01-15 2012-09-10 Закрытое акционерное общество "Научно-исследовательский институт "Аджиномото-Генетика" (ЗАО АГРИ) Способ получения l-аминокислот с использованием бактерий семейства enterobacteriaceae
RU2010101135A (ru) 2010-01-15 2011-07-20 Закрытое акционерное общество "Научно-исследовательский институт "Аджиномото-Генетика" (ЗАО АГРИ) (RU) Бактерия семейства enterobacteriaceae - продуцент l-аспартата или метаболитов, производных l-аспартата, и способ получения l-аспартата или метаболитов, производных l-аспартата
JP2013074795A (ja) 2010-02-08 2013-04-25 Ajinomoto Co Inc 変異型ｒｐｓＡ遺伝子及びＬ−アミノ酸の製造法
RU2471868C2 (ru) 2010-02-18 2013-01-10 Закрытое акционерное общество "Научно-исследовательский институт "Аджиномото-Генетика" (ЗАО АГРИ) Мутантная аденилатциклаза, днк, кодирующая ее, бактерия семейства enterobacteriaceae, содержащая указанную днк, и способ получения l-аминокислот
RU2471870C2 (ru) 2010-06-03 2013-01-10 Закрытое акционерное общество "Научно-исследовательский институт "Аджиномото-Генетика" (ЗАО АГРИ) СПОСОБ ПОЛУЧЕНИЯ L-АРГИНИНА И L-ЦИТРУЛЛИНА С ИСПОЛЬЗОВАНИЕМ БАКТЕРИИ СЕМЕЙСТВА ENTEROBACTERIACEAE, В КОТОРОЙ ОСЛАБЛЕНА ЭКСПРЕССИЯ ГЕНА pepA
RU2010122646A (ru) 2010-06-03 2011-12-10 Закрытое акционерное общество "Научно-исследовательский институт "Аджиномото-Генетика" (ЗАО АГРИ) (RU) Способ получения l-аминокислоты с использованием бактерии семейства enterobacteriaceae, в которой ослаблена экспрессия генов, кодирующих транспортер лизина/аргинина/орнитина
RU2482188C2 (ru) 2010-07-21 2013-05-20 Закрытое акционерное общество "Научно-исследовательский институт "Аджиномото-Генетика" (ЗАО АГРИ) СПОСОБ ПОЛУЧЕНИЯ L-АРГИНИНА С ИСПОЛЬЗОВАНИЕМ БАКТЕРИЙ РОДА Escherichia, В КОТОРОЙ ИНАКТИВИРОВАН ОПЕРОН astCADBE
RU2501858C2 (ru) 2010-07-21 2013-12-20 Закрытое акционерное общество "Научно-исследовательский институт "Аджиномото-Генетика" (ЗАО АГРИ) СПОСОБ ПОЛУЧЕНИЯ L-АМИНОКИСЛОТЫ С ИСПОЛЬЗОВАНИЕМ БАКТЕРИИ СЕМЕЙСТВА Enterobacteriaceae
JP2014036576A (ja) 2010-12-10 2014-02-27 Ajinomoto Co Inc Ｌ−アミノ酸の製造法
RU2011134436A (ru) 2011-08-18 2013-10-27 Закрытое акционерное общество "Научно-исследовательский институт Аджиномото-Генетика" (ЗАО "АГРИ") Способ получения l-аминокислоты с использованием бактерии семейства enterobacteriaceae, обладающей повышенной экспрессией генов каскада образования флагелл и клеточной подвижности
JP2015013812A (ja) 2011-11-01 2015-01-22 味の素株式会社 植物ウイルスの感染抑制剤およびそれを用いた植物ウイルス感染抑制方法
RU2013118637A (ru) 2013-04-23 2014-10-27 Закрытое акционерное общество "Научно-исследовательский институт Аджиномото-Генетика" (ЗАО "АГРИ") СПОСОБ ПОЛУЧЕНИЯ L-АМИНОКИСЛОТ С ИСПОЛЬЗОВАНИЕМ БАКТЕРИИ СЕМЕЙСТВА ENTEROBACTERIACEAE, В КОТОРОЙ РАЗРЕГУЛИРОВАН ГЕН yjjK
PE20150681A1 (es) 2013-05-13 2015-05-15 Ajinomoto Kk Metodo para producir l-aminoacidos
WO2015014829A1 (en) * 2013-07-31 2015-02-05 F. Hoffmann-La Roche Ag Method for the recombinant production of a polypeptide in prokaryotic cells
RU2013140115A (ru) 2013-08-30 2015-03-10 Закрытое акционерное общество "Научно-исследовательский институт Аджиномото-Генетика" (ЗАО "АГРИ") СПОСОБ ПОЛУЧЕНИЯ L-АМИНОКИСЛОТ С ИСПОЛЬЗОВАНИЕМ БАКТЕРИИ СЕМЕЙСТВА Enterobacteriaceae, В КОТОРОЙ НАРУШЕНА ЭКСПРЕССИЯ КЛАСТЕРА ГЕНОВ znuACB
JP2016192903A (ja) 2013-09-17 2016-11-17 味の素株式会社 海藻由来バイオマスからのｌ−アミノ酸の製造方法
JP5958653B2 (ja) 2013-10-02 2016-08-02 味の素株式会社 アンモニア制御装置およびアンモニア制御方法
RU2013144250A (ru) 2013-10-02 2015-04-10 Закрытое акционерное общество "Научно-исследовательский институт Аджиномото-Генетика" (ЗАО "АГРИ") СПОСОБ ПОЛУЧЕНИЯ L-АМИНОКИСЛОТ С ИСПОЛЬЗОВАНИЕМ БАКТЕРИИ СЕМЕЙСТВА Enterobacteriaceae, В КОТОРОЙ ОСЛАБЛЕНА ЭКСПРЕССИЯ ГЕНА, КОДИРУЮЩЕГО ФОСФАТНЫЙ ТРАНСПОРТЕР
JP6459962B2 (ja) 2013-10-21 2019-01-30 味の素株式会社 Ｌ−アミノ酸の製造法
JP6519476B2 (ja) 2013-10-23 2019-05-29 味の素株式会社 目的物質の製造法
RU2015120052A (ru) 2015-05-28 2016-12-20 Аджиномото Ко., Инк. Способ получения L-аминокислоты с использованием бактерии семейства Enterobacteriaceae, в которой ослаблена экспрессия гена gshA
BR112018017227A2 (pt) 2016-02-25 2019-02-05 Ajinomoto Kk método para produzir um l-aminoácido
JP7066977B2 (ja) 2017-04-03 2022-05-16 味の素株式会社 Ｌ－アミノ酸の製造法
WO2020071538A1 (en) 2018-10-05 2020-04-09 Ajinomoto Co., Inc. Method for producing target substance by bacterial fermentation
WO2020138178A1 (en) 2018-12-27 2020-07-02 Ajinomoto Co., Inc. Method for producing basic l-amino acids or salts thereof by fermentation of an enterobacteriaceae bacterium
BR112021014194A2 (pt) 2019-02-22 2021-12-28 Ajinomoto Kk Método para a produção de um l-aminoácido
BR112021017870A2 (pt) 2019-04-05 2021-12-07 Ajinomoto Kk Método para produzir um l-aminoácido
CN111909917B (zh) * 2019-05-10 2022-10-14 中国科学院微生物研究所 一种内溶素Lysmeta1及其编码基因与应用
JP2022550084A (ja) 2019-09-25 2022-11-30 味の素株式会社 細菌の発酵によるｌ－アミノ酸の製造方法
WO2021133030A1 (ko) * 2019-12-23 2021-07-01 씨제이제일제당 (주) 사이토크롬 c 활성이 강화된 l-아미노산 생산 미생물 및 이를 이용한 l-아미노산 생산방법
CN113106075B (zh) * 2021-02-25 2022-06-14 齐鲁工业大学 一种细胞色素氧化酶突变体及其应用
JP2024003706A (ja) * 2022-06-27 2024-01-15 花王株式会社 芳香族化合物の製造方法

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4104124A (en) * 1976-08-30 1978-08-01 Louisiana State University Foundation Process for the production of single cell protein and amino acids
US5175108A (en) * 1990-08-30 1992-12-29 Degussa Aktiengesellschaft Plasmids from corynebacterium glutamicum and plasmid vectors derived therefrom
US5830716A (en) * 1993-10-28 1998-11-03 Ajinomoto Co., Inc. Increased amounts of substances by modifying a microorganism to increase production of NADPH from NADH
WO1999046363A1 (en) 1998-03-11 1999-09-16 Valtion Teknillinen Tutkimuskeskus Transformed microorganisms with improved properties
EP0967282A2 (en) 1998-06-11 1999-12-29 Ajinomoto Co., Inc. Cytochrome bd type quinol oxidase gene of Brevibacterium lactofermentum
US20020106800A1 (en) * 2000-09-28 2002-08-08 Liaw Hungming J. Escherichia coli strains which over-produce L-thereonine and processes for the production of L-threonine by fermentation
US20050221455A1 (en) * 2003-10-21 2005-10-06 Cargill, Inc. Production of monatin and monatin precursors

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6074830A (en) * 1998-06-09 2000-06-13 E. I. Du Pont De Nemours & Company 3,4-dihydroxy-2-butanone 4-phosphate synthase

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4104124A (en) * 1976-08-30 1978-08-01 Louisiana State University Foundation Process for the production of single cell protein and amino acids
US5175108A (en) * 1990-08-30 1992-12-29 Degussa Aktiengesellschaft Plasmids from corynebacterium glutamicum and plasmid vectors derived therefrom
US5830716A (en) * 1993-10-28 1998-11-03 Ajinomoto Co., Inc. Increased amounts of substances by modifying a microorganism to increase production of NADPH from NADH
WO1999046363A1 (en) 1998-03-11 1999-09-16 Valtion Teknillinen Tutkimuskeskus Transformed microorganisms with improved properties
EP0967282A2 (en) 1998-06-11 1999-12-29 Ajinomoto Co., Inc. Cytochrome bd type quinol oxidase gene of Brevibacterium lactofermentum
US20020106800A1 (en) * 2000-09-28 2002-08-08 Liaw Hungming J. Escherichia coli strains which over-produce L-thereonine and processes for the production of L-threonine by fermentation
US20050221455A1 (en) * 2003-10-21 2005-10-06 Cargill, Inc. Production of monatin and monatin precursors

Non-Patent Citations (27)

* Cited by examiner, † Cited by third party
Title
Alessandro Giuffre, et al., Electron Transfer Kinetics of caa3 Oxidase from Bacilllus stearothermophilus a Hypothesis of Thermophilicity, Biophysical Journal, vol. 76, Jan. 1999. pages 438-442.
Bott and Niebisch, The respiratory chain of Corynebacterium glutamicum, J Biotechnology, 2003, vol. 104, pp. 129-153. *
Calhoun et al, Energetic efficiency of Escherichia coli: effects of mutations in components of the aerobic respiratory chain, J Bacteriol. May 1993; 175(10): 3020-3025. *
Castresana and Saraste, Evolution of energetic metabolism: the respiration-early hypothesis, TIBS, 1995, vol. 20, pp. 443-448. *
Castresana, J. Comparative genomics and Bioenergetics, Biochimica et Biophysica Acta, 2001, 1506,pp. 147-162. *
Ching-Ping Tseng, et al., Journal of Bacteriology, vol. 178, No. 4, pp. 1094-1098, "Effect of Microaerophilic Cell Growth Conditions on Expression of the Aerobic (cyoABCDE and cydAB) and Anaerobic (narGHJI, frdABCD, and dmsABC) Respiratory Pathway Genes in Escherichia coli", Feb. 1996.
Collection of Summaries of Lectures made at the Meeting of Japan Bioengineering Association, Sep. 15, 1995, p. 105, with English translation thereof.
DT Ciccognani et al., FEMS Microbiology Letters,"Carbon monoxide-binding properties of the cytochrome bo quinol oxidase complex in Escherichia coli are changed by copper deficiency in continuous culture," 1992, 94, 1-6. *
I. G. Young, et al., Eur. J. Biochem., vol. 116, pp. 165-170, "Nucleotide Sequence Coding for the Respiratory NADH Dehydrogenase of Escherichia coli", 1981.
J. Bongaerts, et al., Molecular Microbiology, vol, 16, No. 3, pp. 521-534, "Transcriptional Regulation of the Proton Translocating NADH Dehydrogenase Genes (nuoA-N) of Escherichia coli by Electron Acceptors, Electron Donors and Gene Regulators", 1995.
J. Green, et al., Molecular Microbiology, vol. 12, No. 3, pp. 433-444, "Regulation of Trnscription at the NDH Promoter of Escherichia coli by FNR and Novel Factors", 1994.
J. Minagawa, et al., The Journal of Biological Chemistry, vol. 265, No. 19, pp. 11198-11203, "Transcriptional Regulation of the Cytochrome B562-O Complex in Escherichia coli", Jul. 5,1990.
JE Bailey, Science, "Toward a Science of Metabolic Engineering," Jun. 1991, vol. 252, pp. 1668-1675. *
Junshi Sakamoto, et al., Cytochrome c Oxidase Contains an Extra Charged Amino Acid Cluster in a New Type of Respiratoroy Chain in the Amino-acid-producing Gram-positive Bacterium Corynebacterium glutamicum, Microbiologoy, 2001, 147, 2865-2871.
Junshi Sakamoto, et al., Gene Structure and Quinol Oxidase Activity of a Cytochrome bd-type Oxidase from Bacillus sterothermophilus, Biochimica et Biophysica Acta, 1411, 1999, pp. 147-158.
Kuniichiro Kusumoto, et al., vol. 173, No. 5-6, pp. 390-397, "Menaquinol Oxidase Activity and Primary Structure of Cytochrome BDFrom the Amino-Acid Fermenting Bacterium Corynebacterium glutamicum", May 2000.
Kusomoto et al, Menaquinol oxidase activity and primary structure of cytochrome bd from the amino-acid fermenting bacterium Corynebacterium glutamicum,Arch Microbiol (2000) 173 :390-397. *
Lena Winstedt, et al., Cytochrome bd Biosynthesis in Bacillus subtilis: Characterization of the cydABCD Operon, Journal of Bacteriology, vol. 180, No. 24, Dec. 1998, pp. 6571-6580.
M. W. Calhoun, et al., Journal of Bacteriology, vol. 175, No. 10, pp. 3020-3025, "Energetic Efficiency of Escherichia coli: Effects of Mutations in Components of the Aerobic Respiratory Chain", May 1993.
Margarida Santana, et al.. Molecular Cloning, Sequencing, and Physiological Characterization of the auox Operon from Bacillus subtilis Encoding the aa3-600 Quinol Oxidase, The Journal of Biological Chemistry, vol. 267, No. 15, May Issue, 1992, pp. 10225-10231.
Melissa W. Calhoun, et al., Journal of Bacteriology, vol. 175, No. 10, pp. 3020-3025, "Energetic Efficiency of Escherichia Coli: Effects of Mutations in Components of the Aerobic Respiratory Chain", May 1993.
Neijssel and de Mattos. The energetics of bacterial growth: a reassessment. Molecular Microbiology. (1994) 13(2), pp. 179-182. *
Nobuhito Sone, et al., Journal of Biochemistry (Tokyo), vol. 127, No. 4, pp. 551-557, "Energy-Yielding Properties of SOXB-Type Cytochrome BO3 Terminal Oxidase: Analyses Involving Bacillus Stearothermophilus K1041 and Its Mutant Strains1", Apr. 2000.
Nobuhito Sone, et al., Journal of Bioscience and Bioengineering, vol. 87, No. 4, pp. 495-499, "Direct Correlationship Between Proton Translocation and Growth Yield: An Analysis of the Respiratory Chain of Bacillus Stearothermophilus", Apr. 1999.
Parekh et al. Improvement of microbial strains and fermentation processes. Appl Microbiol. Biotechnol. (2000) 54, pp. 287-301. *
Spehr et al, Overexpression of the Escherichia coli nuo-Operon and Isoaltion of the overporduced NADH:Ubiquinone Oxidoreductase (Complex I), Biochemistry, 1999, vol. 38, pp. 16261-16267. *
V. Chepuri, et al., The Journal of Biological Chemistry, vol. 265, No. 19, pp. 11185-11192, "The Sequence of the CYO Operon Indicates Substantial Structural Similarities Between the Cytochrome O Ubiquinol Oxidase of Escherichia coli and the AA3-Type Family of Cytochrome C Oxidases", Jul. 5, 1990.

Also Published As

Publication number Publication date
US20140045219A1 (en) 2014-02-13
KR20020005441A (ko) 2002-01-17
MY127434A (en) 2006-12-29
EP1170376B1 (en) 2009-09-09
DE60144205D1 (de) 2011-04-21
JP4380029B2 (ja) 2009-12-09
KR100805644B1 (ko) 2008-02-26
EP1170376A1 (en) 2002-01-09
DE60139838D1 (de) 2009-10-22
ES2331601T3 (es) 2010-01-11
TWI238192B (en) 2005-08-21
ATE442453T1 (de) 2009-09-15
ATE501265T1 (de) 2011-03-15
AU5416901A (en) 2002-01-10
BR0102666A (pt) 2002-02-26
US20020160461A1 (en) 2002-10-31
PL206590B1 (pl) 2010-08-31
RU2238325C2 (ru) 2004-10-20
AU782560B2 (en) 2005-08-11
DK2067864T3 (da) 2011-06-27
EP2067864A1 (en) 2009-06-10
EP2067864B1 (en) 2011-03-09
CN1335401A (zh) 2002-02-13
CN1280419C (zh) 2006-10-18
PE20020172A1 (es) 2002-03-22
PL348448A1 (en) 2002-01-14
ES2360174T3 (es) 2011-06-01
JP2002017363A (ja) 2002-01-22
DK1170376T3 (da) 2009-12-14
BRPI0102666B1 (pt) 2017-05-02

Similar Documents

Publication Publication Date Title
US8586334B2 (en) Method for producing substance utilizing microorganism
US5830716A (en) Increased amounts of substances by modifying a microorganism to increase production of NADPH from NADH
KR100823044B1 (ko) 트레오닌 및 이소류신의 제조방법
US7335496B2 (en) Method for producing target substance
EP1740694B1 (en) L-tryptophan-producing bacterium and a method for producing l-tryptophan
EP1217076B1 (en) Method of producing a target substance by fermentation
JP3861290B2 (ja) ストレス耐性微生物及び発酵生産物の製造法
US7163810B2 (en) Method for producing target substance
US20050106688A1 (en) Method for producing L-amino acid
US6579699B1 (en) Method for producing fermentative product and stress-resistant microorganism
BamHI S kkkk I

Legal Events

Date Code Title Description
AS Assignment

Owner name: AJINOMOTO CO., INC., JAPAN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:NAKAI, YUTA;NAKANISHI, KAZUO;KAWAHARA, YOSHIO;AND OTHERS;REEL/FRAME:012204/0462

Effective date: 20010619

STCF Information on status: patent grant

Free format text: PATENTED CASE

FPAY Fee payment

Year of fee payment: 4

MAFP Maintenance fee payment

Free format text: PAYMENT OF MAINTENANCE FEE, 8TH YEAR, LARGE ENTITY (ORIGINAL EVENT CODE: M1552); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

Year of fee payment: 8